Removal of microorganisms from fluid samples using nanofiber filtration media

ABSTRACT

A method for removing microorganisms from liquid samples and a nanofiber containing liquid filtration medium that simultaneously exhibits high liquid permeability and high microorganism retention. Microorganisms such as bacteria, particularly  B. Diminuta , are removed from a liquid by passing the liquid through a porous nanofiber containing filtration medium having a  B. Diminuta  LRV greater than about 9, and the nanofiber(s) has a diameter from about 10 nm to about 1,000 nm. Another method for removing microorganisms such as bacteria and  Mycloplasma , includes passing the liquid through a porous nanofiber containing filtration medium having a microorganism LRV greater than about 8, and the nanofiber(s) has a diameter from about 10 nm to about 1,000 nm. The filtration medium can be in the form of a fibrous electro spun polymeric nanofiber liquid filtration medium mat.

CROSS REFERENCED TO RELATED APPLICATIONS

This application is a Continuation of application Ser. No. 15/691,286,which is a Continuation of application Ser. No. 13/257,501, which is theNational Stage of International Application No. PCT/US10/00826 filed onMar. 19, 2010, which claims the benefit of U.S. Provisional Application61/210,468 filed on Mar. 19, 2009. The entire contents of theseapplications are incorporated herein by reference in their entirety.

FILED OF THE INVENTION

The present invention relates generally to filtration media. In certainembodiments, the invention provides a porous electrospun nanofiberliquid filtration mat, and methods of using the same in the retention ofmicroorganism from a filtered liquid.

BACKGROUND OF THE INVENTION

Filters used in liquid filtration can be generally categorized as eitherfibrous nonwoven media filters or porous film membrane filters.

Fibrous nonwoven liquid filtration media include, but are not limitedto, nonwoven media formed from spunbonded, melt blown or spunlacedcontinuous fibers; hydroentangled nonwoven media formed from cardedstaple fiber and the like or some combination of these types. Typically,fibrous nonwoven filter media filters used in liquid filtration havepore sizes generally greater than about 1 micron (μm).

Porous film membrane liquid filtration media is used either unsupportedor used in conjunction with a porous substrate or support. Porousfiltration membranes have pore sizes smaller than the fibrous nonwovenmedia, and typically have pore sizes less than about 1 μm. Porous filmliquid filtration membranes can be used in (a) microfiltration, whereinparticulates filtered from a liquid are typically in the range of about0.1 μm to about 10 μm; (b) ultrafiltration, wherein particulatesfiltered from a liquid, are typically in the range of about 5 nm toabout 0.1 μm; and (c) reverse osmosis, wherein particulate matterfiltered from a liquid, are typically in the range of about 1 Å to about1 nm.

Fibrous nonwoven media and porous film membranes are each suitable foruse in microfiltration. Microfiltration is widely accepted in industryas a reliable, easily scalable, and benign method to removemicroorganisms, such as bacteria, from a fluid stream, and is anessential part of pharmaceutical and biopharmaceutical manufacturing. Itis especially important in the biopharmaceutical industry, wheremicrofiltration is used at multiple locations during biopharmaceuticalprocessing.

However, in order to achieve particle retentions equivalent to poresizes of less than about 1 μm using microfiltration with a fibrousnonwoven media, the number of layers of fibrous material the filterneeds to be increased in order to increase the depth of the nonwovenmedia. Increasing the number of fibrous layers in the nonwoven mediaproduces both desirable and undesirably results. Increasing the numberof fibrous layers produces desirable results by increased tortuosity ofa defect path through which a contaminant particle must pass to escapecapture by the filter media as well as increasing thecontaminant-holding capacity of the filter media. However, increasingthe number of fibrous layers in nonwoven media undesirably increases thepressure drop or differential pressure across the media when in use,which translates to increased energy for the filter user and a shorterfilter lifespan.

Porous membrane filters used in microfiltration, unlike fibrous nonwovenmedia, offer a combination of good particle retention, pressure drop andflux, but also tend to be cost-prohibitive, and typically do not providegood contaminant-holding capacity over the entire range of pressuredrop, therefore limiting the life of filters using porous membranes.

The two most desired features of liquid microfiltration membrane arehigh permeability and reliable retention. Naturally, there is atrade-off between these two parameters, and for the same type ofmembrane, greater retention has historically been achieved bysacrificing permeability of the membrane. The inherent limitations ofthe conventional processes for making membranes prevents membranes fromexceeding a certain threshold in porosity, and thus limits the magnitudeof permeability that can be achieved at a given pore size.

A quantitative measure of microorganism retention by a filtrationmembrane is customarily expressed as a Log Reduction Value, or LRV. LRVis a logarithm of the ratio of particle concentration in the challengesolution to that in the filter effluent:LRV=Log{[CFU]_(challenge)/[CFU]_(effluent)}

In the case when the filter retains all microorganisms under theconditions of the test, it is customarily to report the LRV as greaterthan the value obtained when a single microorganism passes the filter.For example, at the challenge particle concentration of 4.77*10⁷CFU/cm², the maximum measurable LRV is 8.22. When no particles pass thefilter, the LRV is reported as greater than 8.22.

Pore size rating of a membrane is an indicator that the membrane hassuccessfully passed a relevant, standardized bacterial challenge test.The most common pore size rating is 0.22 μm, which is assigned tomembranes that pass a Standard Test Method for Determining BacterialRetention Of Membrane Filters Utilized For Liquid Filtration (ASTMF838-83 test), can be validated to produce sterile effluent after beingchallenged with ≥10⁷ CFU/cm² Brevundimonas diminuta.

Brevundimonas diminuta (ATTC #19146), formerly known as Pseudomonasdiminuta, is an aerobic gram-negative bacteria (bacilli). Because of itssmall size, B. diminuta is a standard microbial organism for validationof membrane filters and the like for sterilization. However, while B.diminuta is representative of most pathogenic bacteria, B. diminuta hasproved to be a poor model for a class of microorganisms calledMycoplasma. While representative of most pathogenic bacteria, B.diminuta has proved to be a poor model for a class of microorganismscalled Mycoplasma.

Mycoplasma is a microorganism that can infect cell cultures and can havea substantially deleterious effect to biopharmaceutical manufacturing.The contamination of eukaryotic cell cultures and the like withMycoplasma is also a common problem, leading to unreliable experimentalresults and possibly unsafe biological products. This represents aserious problem for manufacturers involved in the development andfabrication of biological and pharmaceutical products. The highlynutritive environment of the media used in cell culture can lead to thepropagation of Mycoplasmas, resulting in diminished cell growth as wellas the loss of cultures. In contrast to contamination with types ofbacteria which can be detected in a short period after infection on thebasis of visible effects such as cytopathicity, pH change, abnormalgrowth, the media appearing turbid, contamination caused by Mycoplasmamay go undetected without noticeable symptoms (Razin, S. 1997.Comparative genomics of Mycoplasmas. Wien Klin Wochenschr 109:551-6.Jung H, Wang S Y, Yang I W, Hsuch W, Yang W J, Wang T H, Wang: H S.(2003) Detection and treatment of Mycoplasma contamination in culturedcells, Chang Gung Med J. 26: 250-8 Wisher M. (2002) Biosafety andproduct release testing issues relevant to replication-competentoncolytic viruses, Review, Cancer Gene Ther. 9: 1056-61).

A membrane pore size rating of 0.1 μm indicates that a membrane has beenvalidated to remove Mycoplasma. (See, Roche, K. L.: Levy, R. V., Methodsto Validate Microporous Membranes for the Removal of Mycoplasma,BioPharm 1992, 5, (3), 22-33)

For example, membranes having a pore size rating of 0.1 μm can be usedto filter media, nutrient and cell culture fluid delivered to cellsliving and growing inside of a bioreactor. Membranes currently existthat have a specific Log Reduction Value (LRV) for A. Laidawii, a testmicroorganism for Mycoplasma. While it is customarily accepted thatLRV>8 is sufficient to claim “full” retention of Mycoplasma, filtershaving a lower LRV are often used instead in liquid filtration becauseof greater permeability and higher throughput.

WO/2009/032040, assigned to Millipore Corporation and titled, SERUM-FREEGROWTH MEDIUM FOR ACHOLEPLASMA LAIDLAWII AND METHODS FOR RETENTIONTESTING STERILIZING GRADE FILTERS, fully incorporated by referenceherein in its entirety, teaches the full retention of Mycoplasma by afiltration medium can be validated to produce sterile effluent afterbeing challenged with ≥1 10⁹×cfu/mL Acholeplasma laidlawii (A.laidlawii; ATCC 23206).

For example, two membranes having a pore size rating of 0.1 μm,Durapore® VV and Express SHR, each available from Millipore Corporation,Billeric Mass., USA, have Mycoplasma LRVs of 4 and 6, respectively.While Durapore® MV, also available from Millipore Corporation, claimsfull Mycoplasma retention (LRV>8), it has a lower permeability andcapacity in media filtration compared to Durapore® VV and Express SHR.

Synthetic polymers have been formed into webs of very small diameterfibers, i.e., on the order of a few micrometers or less than 1 μm, usingvarious processes including melt blowing, electrostatic spinning andelectroblowing. Such webs have been shown to be useful as liquid barriermaterials and filters. Often they are combined with stronger sheets toform composites, wherein the stronger sheets provide the strength tomeet the needs of the final filter product.

U.S. Patent Publication Number 2004/0038014 is issued to Schaefer et al.teaches a nonwoven filtration mat comprising one or more layers of athick collection of fine polymeric microfibers and nanofibers formed byelectrostatic spinning for filtering contaminants. The electrostaticspinning process utilizes an electro spinning apparatus including areservoir in which the fine fiber forming polymer solution is contained,a pump and an emitter device which obtains polymer solution from thereservoir. In the electrostatic field, a droplet of the polymer solutionis accelerated by the electrostatic field toward a collecting mediasubstrate located on a grid. A high voltage electrostatic potentialmaintained between the emitter and grid, with the collection substratepositioned there between, by means of a suitable electrostatic voltagesource.

The “electroblowing” process is disclosed in World Patent PublicationNo. WO 03/080905, incorporated herein by reference in its entirety. Astream of polymeric solution comprising a polymer and a solvent is fedfrom a storage tank to a series of spinning nozzles within a spinneret,to which a high voltage is applied and through which the polymericsolution is discharged. Meanwhile, compressed air that is optionallyheated is issued from air nozzles disposed in the sides of, or at theperiphery of the spinning nozzle. The air is directed generally downwardas a blowing gas stream which envelopes and forwards the newly issuedpolymeric solution and aids in the formation of the fibrous web, whichis collected on a grounded porous collection belt above a vacuumchamber. The electroblowing process permits formation of commercialsizes and quantities of nanowebs at basis weights in excess of about 1gsm, even as high as about 40 gsm or greater, in a relatively short timeperiod.

U.S. Patent Publication Number 2007/0075015 issued to Bates et al.teaches a liquid filtration media including at least one layer ofnanofibers having average diameters less than 1,000 nanometersoptionally disposed on scrim layer for filtering particulate matter in aliquid. The filtration media have flow rates of at least 0.055 L/min/cm²at relatively high levels of solidity. The media apparently hasnon-diminishing flow rates as differential pressures increase between 2psi (14 kPa) and 15 psi (100 kPa).

U.S. Patent Publication Number 2007/0018361 issued to Xu teachesfabricating nanofibers by reactive electrospinning, wherein theelectrospinning process is coupled with an in-line reactor wherechemical or photochemical reactions take place. The processes taught inXu use electrospinning to allow for the production of nanofibers fromcrosslinked polymers and other materials.

U.S. Patent Publication Number 2009/0026137 issued to issued to Chenteaches fabricating liquid filter with a composite medium that has ananoweb adjacent to and optionally bonded to a microporous membrane. Themembrane is characterized by an LRV value of 3.7 at a rated particlesize, and the nanoweb has a fractional filtration efficiency of greaterthan 0.1 at the rated particle size of the membrane. The nanoweb alsohas a thickness efficiency ratio of greater than 0.0002 at thatefficiency. The nanoweb acts to provide depth filtration to themembrane.

It would be desirable to have a reliable electrospun nanofiber liquidfiltration medium having a microorganism LRV greater than about 8,suitable for full retention of microorganisms such as bacteria,Mycoplasma in particular, and/or a B. Diminuta LRV greater than about 9,suitable for full retention of B. Diminuta, when removed from a liquidpassing through the filtration medium, while simultaneously achievinghigh permeability and high throughput.

Additionally, the porous electrospun nanofiber filtration medium wouldbe readily scalable, adaptable to processing volumes of sample fluidsranging from milliliters to thousands of liters, and capable of use witha variety of filtration processes and devices. The invention is directedto these, as well as other objectives and embodiments.

SUMMARY OF THE INVENTION

The present invention is directed to a method of removing microorganismsfrom a liquid by passing the liquid through a porous electrospunnanofiber liquid filtration medium. The electrospun nanofiber liquidfiltration medium can be used with or without being disposed on a poroussupport or substrate. The electrospun nanofiber liquid filtration mediumcan be formed into a variety of shapes, sizes, thicknesses anddensities, such as a porous, polymeric nanofiber mat.

In another embodiment, the present invention is directed towards porous,electrospun nanofiber liquid filtration medium having a B. Diminuta LRVgreater than about 9, and the nanofiber(s) has an average fiber diameterranging from about 10 nm to about 1000 nm.

In another embodiment, the present invention is directed towards aporous electrospun nanofiber liquid filtration medium having a B.Diminuta LRV greater than about 9, and the filtration medium has aporosity ranging from about 80% to about 95%.

In another embodiment, the present invention is directed towards aporous electrospun nanofiber liquid filtration medium having aMycoplasma LRV greater than about 4, and a liquid permeability at 10 psidifferential pressure greater than about 3,000 LMH. (Liters Per SquareMeter Per Hour).

In another embodiment, the present invention is directed towards aporous electrospun nanofiber liquid filtration medium having aMycoplasma LRV greater than about 8, and a liquid permeability at 10 psidifferential pressure greater than about 3,000 LMH.

In another embodiment, the present invention is directed towards aporous electrospun nanofiber liquid filtration medium having a B.Diminuta LRV greater than about 9, and formed as a fibrous porous mathaving a thickness ranging from about 1 μm to about 500 μm.

In another embodiment, the present invention is directed towards aporous electrospun nanofiber liquid filtration medium having a B.Diminuta LRV greater than about 9, and a liquid permeability at 10 psidifferential pressure greater than about 10,000 LMH.

In another embodiment, the present invention is directed towards aporous electrospun nanofiber liquid filtration medium having aMycoplasma LRV greater than about 8, and the nanofiber(s) has an averagefiber diameter ranging from about 10 nm to about 1,000 nm.

In another embodiment, the present invention is directed towards aporous electrospun nanofiber liquid filtration medium having aMycoplasma LRV greater than about 8, and a liquid permeability at 10 psidifferential pressure greater than about 3,000 LMH.

In another embodiment, the present invention directed towards a porouselectrospun nanofiber liquid filtration medium having a Mycoplasma LRVgreater than about 8, and the filtration medium has a porosity rangingfrom about 80% to about 95%.

In another embodiment, the present invention is directed towards aporous electrospun nanofiber liquid filtration medium having aMycoplasma LRV greater than about 8, and formed as a fibrous porous mathaving a thickness ranging from about 1 μm to about 500 μm.

In another embodiment, the present invention is directed towards aporous electrospun nanofiber liquid filtration medium having aMycoplasma LRV greater than about 8, and a liquid permeability at 10 psidifferential pressure greater than about 10,000 LMH.

In another embodiment, the present invention is directed to a processfor forming a porous filtration medium from one or more electrospunpolymeric nanofibers from a polymer solution by using an electrospinningapparatus, and subjecting the solution to an electric potential greaterthan about 10 kV, and collecting electrospun polymer fiber(s) as anon-woven mat.

In another embodiment, the present invention is directed to a compositeporous filtration device comprising a filtration medium having amicroorganism LRV greater than about 8, and including an electrospunpolymeric nanofiber mat disposed on a porous support or poroussubstrate.

Additional features and advantages of the invention will be set forththe detailed description and claims, which follows. Many modificationsand variations of this invention can be made without departing from itsspirit, and scope, as will be apparent to those skilled in the art. Itis to be understood that the foregoing general description and thefollowing detailed description, the claims, as well as the appendeddrawings are exemplary and explanatory only, and are intended to providean explanation of various embodiments of the present teachings. Thespecific embodiments described herein are offered by way of example onlyand are not meant to be limiting in any way.

BRIEF DESCRIPTION OF THE DRAWINGS

The accompanying drawings, which are incorporated in and constitute apart of this specification, illustrate the presently contemplatedembodiments of the invention and, together with the description, serveto explain the principles of the invention.

FIG. 1 is a schematic of the process of electrospinning a nonfiberaccording to one embodiment of the invention. Polymer solution 10,rotating drum 20, moving collecting belt 30, ground electrode 35, highvoltage source 40, polymer fibers produced by electric field 50, fibermat 60 formed from polymer fibers.

FIG. 2 is a cross-sectional scanning electron micrograph of nylon fibersfrom an embodiment of the invention exemplified in Example 1.

FIG. 3 is a frontal scanning electron micrograph of nylon fibers from anembodiment of the invention exemplified in Example 1.

FIG. 4 is a scanning electron micrograph of nylon fibers from anotherembodiment of the invention as exemplified in Example 2.

FIG. 5 is a scanning electron micrograph of a symmetrical commercialmembrane Durapore® MVPP from Comparative Example 1.

FIG. 6 is a scanning electron micrograph of a symmetrical commercialmembrane Durapore® GVPP from Comparative Example 2.

DESCRIPTION OF THE EMBODIMENTS

All publications, patents end patent applications cited herein, whethersupra or infra, are hereby incorporated by reference in their entiretyto the same extent as if each individual publication, patent or patentapplication was specifically and individually indicated to beincorporated by reference.

For the purposes of this specification and appended claims, unlessotherwise indicated, all numbers expressing quantities of ingredients,percentages or proportions of materials, reaction conditions, and othernumerical values used in the specification and claims, are to beunderstood as being modified in all instances by the term “about”.

Accordingly, unless indicated to the contrary, the numerical parametersset forth in the following specification and attached claims areapproximations that may vary depending upon the desired propertiessought to be obtained by the present invention. At the very least, andnot as an attempt to limit the application of the doctrine ofequivalents to the scope of the claims, each numerical parameter shouldat least be construed in light of the number of reported significantdigits and by applying ordinary rounding techniques.

Notwithstanding that the numerical ranges and parameters setting forththe broad scope of the invention are approximations, the numericalvalues set forth in the specific examples are reported as precisely aspossible. Any numerical value, however, inherently contains certainerrors necessarily resulting from the standard deviation found in theirrespective testing measurements. Moreover, all ranges disclosed hereinare to be understood to encompass all subranges subsumed therein. Forexample, a range of “1 to 10” includes any and all subranges between(and including) the minimum value of 1 and the maximum value of 10, thatis, any and all subranges having a minimum value of equal to or greaterthan 1 and a maximum value of equal to or less than 10, e.g., 5.5 to 10.

Before describing the present invention in further detail, a number ofterms will be defined. Use of these terms does not limit the scope ofthe invention but only serve to facilitate the description of theinvention.

As used herein, the singular forms “a,” “an” and “the” include pluralreferents unless the context clearly dictates otherwise.

The term “nanofibers” refers to fibers having diameters varying from afew tens of nanometers up to several hundred nanometers, but generallyless than one micrometer.

The terms “filter medium” or “filter media” refer to a material, orcollection of material, through which a fluid carrying a microorganismcontaminant passes, wherein microorganism is deposited in or on thematerial or collection of material.

The terms “flux” and “flow rate” are used interchangeably to refer tothe rate at which a volume of fluid passes through a filtration mediumof a given area.

The filtration medium of the present invention includes a porouselectrospun nanofiber liquid filtration mat. The nanofibers have anaverage fiber diameter of about 10 nm to about 1000 nm. The filtrationmedium has a mean pore size ranging from about 0.1 μm to about 1 μm. Thefiltration medium has a porosity ranging from about 80% to about 95%.The filtration medium has a thickness ranging from about 1 μm to about500 μm, preferably from about 50 μm and about 200 μm. The filtrationmedium has liquid permeability greater than about 300 LMH/psi.

Polymers suitable for use in the nanofibers of the invention includethermoplastic and thermosetting polymers. Suitable polymers include, butare not limited to, nylon, polyimide, aliphatic polyamide, aromaticpolyamide, polysulfone, celluose, cellulose acetate, polyether sulfone,polyurethane, poly(urea urethane), polybenzimidazole, polyetherimide,polyacrylonitrile, poly(ethylene terephthalate), polypropylene,polyaniline, poly(ethylene oxide), poly(ethylene naphthalate),poly(butylene terephthalate), styrene butadiene rubber, polystyrene,poly(vinyl chloride), poly(vinyl alcohol), poly(vinylidene fluoride),poly(vinyl butylene), copolymers, derivative compounds and blendsthereof, and combinations thereof.

The process for making the electrospun nanofiber mat of the filtrationmedium is disclosed in WO 2005/024101; WO 2006/131081; and WO2008/106903, all assigned to Elmarco S.R.O., of Liberec, Czech Republic.

In one embodiment of the present invention, the filtration mediumcomprises a mat made from a single nanofiber, wherein the singlenanofiber is made by a single pass of a moving collection apparatuspositioned between the spinning drum and the collector through theprocess. It will be appreciated that the fibrous web can be formed byone or more spinning drums running simultaneously above the same movingcollection apparatus.

In one embodiment of the invention, a fibrous mat is made by depositingnanofiber (s) from a nylon solution. The nanofiber mat has a basisweight of between about 5 g/m² and about 15 g/m², as measured on a drybasis, i.e., after the residual solvent has evaporated or been removed.

As depicted in FIG. 1, a moving collection apparatus 30 is preferably amoving collection belt positioned within the electrostatic field betweenthe spinning beam 20 and the collector 35, wherein the porous mat madefrom a single nanofiber is collected.

In one embodiment of the invention, any of a variety of porous single ormultilayered substrates or supports can be arranged on a movingcollection belt to collect and combine with the electrospun nanofibermat medium, forming a composite filtration device.

Examples of single or multilayered porous substrates or supportsinclude, but are not limited to, spunbonded nonwovens, meltblownnonwovens, needle punched nonwovens, spunlaced nonwovens, wet laidnonwovens, resin-bonded nonwovens, woven fabrics, knit fabrics, paper,and combinations thereof.

In another embodiment of the invention the electrospun the nanofiber matmedium taught herein may be bonded a porous substrate or support.Bonding may be accomplished by known methods in the art, including butnot limited to thermal calendaring between heated smooth nip rolls,ultrasonic bonding, and through gas bonding. Bonding increases thestrength and the compression resistance of the medium so that the mediummay withstand the forces associated with being handled, being formedinto a useful filter, and being used in a filter, and depending on thebonding method used, adjusts physical properties such as thickness,density, and the size and shape of the pores.

For instance, thermal calendering can be used reduce the thickness andincrease the density and reduce the porosity of the electrospunnanofiber mat medium, and reduce the size of the pores. This in turndecreases the flow rate through the medium at a given applieddifferential pressure. In general, ultrasonic bonding will bond to asmaller area of the electrospun nanofiber mat medium than thermalclendering, and therefore has a lesser effect on thickness, density andpore size. Though gas bonding generally has minimal effect on thickness,density and pore size, therefore this bonding method may be preferablein applications in which maintaining higher fluid flow rate is desired.

When thermal calendering is used, care must be taken not to over-bondthe electrospun nanofiber material, such that the nanofibers melt and nolonger retain their structure as individual fibers. In the extreme,over-bonding would result in the nanofibers melting completely such thata film would be formed. One or both of the nip rolls used is heated to atemperature of between about ambient temperature, e.g., about 25° C. andabout 300° C. The nanofiber mat(s) and/or porous support or substrate,can be compressed between the nip rolls at a pressure ranging from about0 lb/in to about 1000 lb/in (178 kg/cm). The nanofiber mat(s) can becompressed at a line speed of at least about 10 ft/min (3 m/min).

Calendering conditions, e.g., roll temperature, nip, pressure and linespeed, can be adjusted to achieve the desired solidity. In general,application of higher temperature, pressure, and/or residence time underelevated temperature and/or pressure results in increased solidity.

Other mechanical steps, such as stretching, cooling, heating, sintering,annealing, reeling, unreeling, and the like, may optionally be includedin the overall process of forming, shaping and making the electrospunnanofiber mat medium as desired.

For example, the electrospun nanofiber mat medium taught herein may bestretched in a single step or a plurality of steps as desired. Dependingon the stretching method used to stretch the electrospun nanofiber matmedium, stretching can adjust the physical properties of the matincluding thickness, density, and the size and shape of the pores formedin the mat. For example, if the electrospun nanofiber mat is stretchedin a single direction (uniaxial stretching), the stretching may beaccomplished by a single stretching step or a sequence of stretchingsteps until the desired final stretch ratio is attained.

Similarly, if the electrospun nanofiber mat medium is stretched in twodirections (biaxial stretching), the stretching can be conducted by asingle biaxial stretching step or a sequence of biaxial stretching stepsuntil the desired final stretch ratios are attained. Biaxial stretchingmay also be accomplished by a sequence of one or more uniaxialstretching steps in one direction and one or more uniaxial stretchingsteps in another direction. Biaxial stretching steps where theelectrospun nanofiber mat is stretched simultaneously in two directionsand uniaxial stretching steps may be conducted in sequence in any order.

Methods for stretching the mat are not particularly limited, and use maybe made of ordinary tentering, rolling, or inflation or a combination oftwo or more of these. The stretching may be conducted uniaxially,biaxially, etc. In the case of biaxial stretching, machine-directionstretching and transverse-direction stretching may be conducted eithersimultaneously or successively.

Various types of stretching apparatus are well known in art and may beused to accomplish stretching of the electrospun mat according to thepresent invention. Uniaxial stretching is usually accomplished bystretching between two rollers wherein the second or downstream rollerrotates at a greater peripheral speed than the first or upstream roller.Uniaxial stretching can also be accomplished on a standard tenteringmachine.

Biaxial stretching may be accomplished by simultaneously stretching intwo different directions on a tentering machine. More commonly, however,biaxial stretching is accomplished by first uniaxially stretchingbetween two differentially rotating rollers as described above, followedby either uniaxially stretching in a different direction using a tentermachine or by biaxially stretching using a tenter machine. The mostcommon type of biaxial stretching is where the two stretching directionsare approximately at right angles to each other. In most cases where acontinuous sheet is being stretched, one stretching direction is atleast approximately parallel to the long axis of the sheet (machinedirection) and the other stretching direction is at least approximatelyperpendicular to the machine direction and is in the plane of the sheet(transverse direction).

After the electrospun nanofiber mat has been stretched either uniaxiallyor biaxially, the stretched porous electrospun nanofiber mat can againbe calendared. The stretched electrospun nanofiber mat can be forwardedto a pair of heated calendar rolls acting cooperatively so as to form amat of reduced thickness compared to the mat exiting from the stretchingapparatus. By regulating the pressure exerted by these calendar rollsalong with the temperature, the pore size of the final electrospunnanofiber mat can be controlled as desired, thereby allowing for theadjustment of the average pore size.

The electrospun nanofiber mat may be heated by any of a wide variety oftechniques prior to, during, and/or after stretching. Examples of thesetechniques include radiative heating such as that provided byelectrically heated or gas fired infrared heaters, convective heatingsuch as that provided by recirculating hot air, and conductive heatingsuch as that provided by contact with heated rolls. The temperatureswhich are measured for temperature control purposes may vary accordingto the apparatus used and personal preference.

In general, the temperature or temperatures can be controlled such thatthe electrospun nanofiber mat is stretched about evenly so that thevariations, if any, in thickness of the stretched mat are withinacceptable limits and so that the amount of stretched microporouselectrospun nanofiber mat outside of those limits is acceptably low. Itwill be apparent that the temperatures used for control purposes may ormay not be close to those of the electrospun nanofiber mat itself sincethey depend upon the nature of the apparatus used, the locations of thetemperature-measuring devices, and the identities of the substances orobjects whose temperatures are being measured.

The porosity can be modified as a result of calendering. The range ofporosity from about 5% to about 90% can be obtained.

While filtration medium is often used in single-layer configuration, itis sometimes advantageous to provide more than one layer of filtrationmedium adjacent to each other. Layering membrane filters to improveparticle retention is commonly used in virus filtration and is practicedcommercially its Millipore's product lines of Viresolve® NFP andViresolve Pro®. Layering filtration media of the same or differentcomposition is also used to improve filter throughput. Examples of suchlayered filters are Millipore's Express® SHC and SHRP product lines.Other considerations for choosing a multi-layered filtration productinclude economics and convenience of media and device manufacturing,ease of sterilization and validation. The fibrous filtration, media ofthe present invention can be used in single-layer or in a multi-layerconfiguration.

Test Methods

Basis Weight was determined by ASTM D-3776, which is hereby incorporatedby reference and reported in g/m².

Porosity was calculated by dividing the basis weight of the sample ing/m² by the polymer density in g/cm³, by the sample thickness inmicrometers, multiplying by 100, and subtracting the resulting numberfrom 100 porosity=100−[basisweight/(density·times·thickness)·times·100].

Fiber Diameter was determined as follows. Ten scanning electronmicroscope (SEM) images at 40,000·times. Magnification was taken of eachnanofiber layer sample. The diameter of ten (10) clearly distinguishablenanofibers were measured from each SEM image and recorded. Defects werenot included lumps of nanofibers, polymer drops, intersections ofnanofibers). The average fiber diameter for each sample was calculated.

Thickness was determined by ASTM D1777-64, which is hereby incorporatedby reference, and is reported in micrometers.

Mean flow bubble point was measured according to ASTM Designation E1294-89, “Standard Test Method for Pore Size Characteristics of MembraneFilters Using Automated Liquid Porosimeter” by using automated bubblepoint method from ASTM Designation F 316 using a custom-built capillaryflow porosimeter, in principle similar to a commercial apparatus fromPorous Materials, Inc, (PMI), Ithaca, N.Y. Individual samples of 47 mmin diameter (9.6 cm² measurable area) were wetted with isopropylalcohol. Each sample was placed in a holder, and a differential pressureof air was applied and the fluid removed from the sample. Thedifferential pressure at which wet flow is equal to one-half the dryflow (flow without wetting solvent) is used to calculate the moan flowpore size using supplied software.

Flow Rate (also referred to as Flux) is the rate at which fluid passesthrough the sample of a given area and was measured by passing deionizedwater through filter medium samples having a diameter of 35 mm. Thewater was forced through the samples using hydraulic pressure (waterhead pressure) or pneumatic pressure (air pressure over water).

The effective pore size of an electrospun mat can be measured usingconventional membrane techniques such as bubble point, liquid-liquidporometry, and challenge test with particles of certain size. It isknown that the effective pore size of a fibrous mat generally increaseswith the fiber diameter and decreases with porosity.

Bubble point test provides a convenient way to measure effective poresize. It is calculated from the following equation:

${P = {\frac{2\gamma}{r}\cos\mspace{11mu}\theta}},$where P is the bubble point pressure, γ is the surface tension of theprobe fluid, r is the pore radius, and θ is the liquid-solid contactangle.

Membrane manufacturers assign nominal pore size ratings to commercialmembrane filters, which are based on their retention characteristics.

While it is known that the pore size distribution of a random non-wovenmat becomes narrower as thickness of the mat increases (See, Meltzer, T.H., In Filtration in the Pharmaceutical Industry, Marcel Dekker: NewYork, 1987; p 103) it has not been previously shown whether the poresize distribution of a non-woven mat can be sufficiently narrow toaccomplish “full bacteria retention” (as discussed supra) at competitivepermeability of at least 100 LMH/psi for Mycoplasma-retentive filtersand 500 LMH/psi for B. Diminuta-retentive filters.

Mycoplasma retention was measured by challenging the membranes with8.77*10⁷ colony forming units per square cm of membrane (CFU/cm²). Thedevices are challenged with 50 mL of diluted A. laidlawii and thenflushed with 50 mL of Mycoplasma Buffer for a total of 100 mL. The full100 mL was then filtered through a 022 μm sterilization membrane. Then,the procedure described in a published patent application WO 2009/032040was followed.

B. Diminuta retention was measured in accordance with ASTM F883-83.

The following Examples of the present invention will demonstrate that anelectrospun nanofiber mat can possess both high permeability and highbacteria retention at the same time.

Hereinafter the present invention will be described in more detail inthe following examples. The invention will be further clarified by thefollowing examples which are intended to be exemplary of the invention.

EXAMPLES Example 1

An electrospinning process and apparatus for forming a nanofiber web asdisclosed in WO 2006/131081 was used to produce the nanofiber layers andmats of the Examples below.

Nanofiber layers were made by electrospinning a solution of Nylon 6polymer. Nylon 6 was supplied by BASF Corp., Florham Park, N.J., USA,under the trademark Ultramid B24. A solvent mixture of acetic and formicacid, weight ratio 2:1, was used to prepare solutions of Nylon, withconcentrations ranging from 8 to 16%.

A 10 wt % solution of Nylon was electrospun at 82 kV and distancebetween solution and ground electrode 155 mm, for 45 minutes. By way ofexample only, samples were tested for A. Laidiawii retention usingstandard Millipore procedures described above. A representative sampleis compared to the closest Durapore® membrane, MVPP, in Table I below.

The results are shown in Table I below.

TABLE I Mean flow bubble Nominal pore Thickness Permeability point forIPA size rating Porosity A. Laidlawii (micron) (LMH/psi) (psi) (micron)(%) LRV Example 1: Electrospun 140 400 65 N/A 88 >8.6 Nylon 140Comparative Example 1: 125 80 55 0.1 70 >8.6 Millipore Durapore ® MVPP

Example 2

A series of Nylon 6 electrospun fibrous mats were prepared as describedin Example 1. A 13 wt. % solution of Nylon was electrospun at 82 kV anddistance between solution and ground electrode 155 mm, for 10 and 45minutes. Fiber mats of 55 and 225 microns thick were produced for thetwo spin times, respectively. These samples were tested, by way ofexample only, for B. Diminuta retention. It should be noted that theMycoplasma-retentive electrospun fibrous mats as taught herein are usedfor the full retention of B. Diminuta.

Example 3

Another series of Nylon 6 electrospun fibrous mats were prepared asdescribed in Example 2. A 16 wt % solution of Nylon was electrospun at82 kV and distance between solution and ground electrode 155 mm, for 15minutes. These samples were tested, by way of example only, for B.Diminuta retention.

The results are shown in Table II below.

TABLE II Mean flow bubble Nominal pore Thickness Permeability point forIPA size rating Porosity B. Diminuta (micron) (LMH/psi) (psi) (micron)(%) LRV Example 2: Nylon 225 225 1,814 33 N/A 90 >9 Example 2: Nylon 5555 4,960 26 N/A 90 >9 Example 3: Nylon 55 160 3,354 13.7 N/A 90 5.5Comparative Example 2: 125 500 30 0.22 75 >9 Millipore Durapore ® GVPP

A higher porosity of electrospun nanofiber mats results in greaterpermeability, while still providing a reliable means for retention ofmicroorganisms.

Method of Use

Electrospun nanofiber containing liquid filtration media, in accordancewith the present invention are useful in the food, beverage,pharmaceuticals, biotechnology, microelectronics, chemical processing,water treatment, an other liquid treatment industries.

Electrospun nanofiber containing liquid filtration media, in accordancewith the present invention may be used for filtering, separating,identifying, and/or detecting microorganisms from a liquid sample orstream.

Electrospun nanofiber containing liquid filtration media, in accordancewith the present invention may be used with any liquid samplepreparation methods including, but not limited to, chromatography; highpressure liquid chromatography (HPLC); electrophoresis; gel filtration;sample centrifugation; on-line sample preparation; diagnostic kitstesting; diagnostic testing; high throughput screening; affinity bindingassays; purification of a liquid sample; size-based separation of thecomponents of the fluid sample; physical properties based separation ofthe components of the fluid sample; chemical properties based separationof the components of the fluid sample; biological properties basedseparation of the components of the fluid sample; electrostaticproperties based separation of the components of the fluid sample; and,combinations thereof. Also, electrospun nanofiber containing liquidfiltration media, in accordance with the present invention can becomponent or part of a larger device and/or system.

Kits

The invention also provides kits which may be used to removemicroorganisms from a liquid sample. The kit may comprise, for example,one or more electrospun nanofiber containing liquid filtration medium inaccordance with the present invention, as well as one or more liquidfiltration devices, support or substrate for the medium. The kit maycontain one or more controls, and may optionally include various buffersuseful in the methods of practicing the invention. Wash buffers foreliminating reagents or eliminating non-specifically retained or boundmaterial may optionally be included in the kit.

Other optional kit reagents include an elution buffer. Each of thebuffers may be provided in a separate container as a solution.Alternatively the buffers may be provided in dry form or as a powder andmay be made up as a solution according to the user's desiredapplication. In this case the buffers may be provided in packets. Thekit may provide a power source in instances where the device isautomated as well as a means of providing an external force such as avacuum pump. The kit may also include instructions for using theelectrospun nanofiber containing liquid filtration medium, device,support or substrate, and/or for making up reagents suitable for usewith the invention, and methods of practicing invention. Optionalsoftware for recording and analyzing data obtained while practicing themethods of the invention or while using the device of the invention mayalso be included.

The term “kit” includes, for example, each of the components combined ina single package, the components individually packaged and soldtogether, or the components presented together in a catalog (e.g., onthe same page or double-page spread in the catalog).

The disclosure set forth above may encompass multiple distinctinventions with independent utility. Although each of these inventionshas been disclosed in its preferred form(s), the specific embodimentsthereof as disclosed and illustrated herein are not to be considered ina limiting sense, because numerous variations are possible. The subjectmatter of the inventions includes all novel and nonobvious combinationsand subcombinations of the various elements, features, functions, and/orproperties disclosed herein. The following claims particularly point outcertain combinations and subcombinations regarded as novel andnonobvious. Inventions embodied in other combinations andsubcombinations of features, functions, elements, and/or properties maybe claimed in applications claiming priority from this or a relatedapplication. Such claims, whether directed to a different invention orto the same invention, and whether broader, narrower, equal, ordifferent in scope to the original claims, also are regarded as includedwithin the subject matter of the inventions of the present disclosure.

We claim:
 1. A filtration device comprising a porous nanofibercontaining filtration medium made by electrospinning a polymer, whereinthe filtration medium exhibits full retention of Brevundimonas diminutaby size-based separation as measured in accordance with ASTM F838-83 anda liquid permeability greater than about 1000 LMH/psi, wherein thenanofiber has a fiber diameter from about 10 nm to about 1,000 nm. 2.The filtration device of claim 1, wherein the filtration medium has athickness ranging from about 1 μm to about 500 μm.
 3. The filtrationdevice of claim 1, wherein the polymer is selected from the groupconsisting of polyimide, aliphatic polyamide, aromatic polyamide,polysulfone, cellulose acetate, polyether sulfone, polyurethane,poly(urea urethane), polybenzimidazole, polyetherimide,polyacrylonitrile, poly(ethylene terephthalate), polypropylene,polyaniline, poly(ethylene oxide), poly(ethylene naphthalate),poly(butylene terephthalate), styrene butadiene rubber, polystyrene,poly(vinyl chloride), poly(vinyl alcohol), poly(vinylidene fluoride),poly(vinyl butylene) and copolymers, derivative compounds, or blendsthereof.
 4. The filtration device of claim 1, wherein the polymercomprises an aliphatic polyamide.
 5. The filtration device of claim 1,wherein the polymer comprises a blend of polymers or copolymers.
 6. Thefiltration device of claim 1, wherein the electrospun nanofibers aredisposed on a porous support.
 7. The filtration device of claim 6,wherein the porous support comprises one or more layers selected fromthe group consisting of spunbonded nonwovens, meltblown nonwovens,needle punched nonwovens, spunlaced nonwovens, wet laid nonwovens,resin-bonded nonwovens, woven fabrics, knit fabrics, paper, andcombinations thereof.
 8. The filtration device of claim 1, wherein thefiltration medium has a porosity from about 80% to about 95%.
 9. Thefiltration device of claim 8, wherein the filtration medium has athickness ranging from about 1 μm to about 500 μm.
 10. The filtrationdevice of claim 8, wherein the polymer is selected from the groupconsisting of polyimide, aliphatic polyamide, aromatic polyamide,polysulfone, cellulose acetate, polyether sulfone, polyurethane,poly(urea urethane), polybenzimidazole, polyetherimide,polyacrylonitrile, poly(ethylene terephthalate), polypropylene,polyaniline, poly(ethylene oxide), poly(ethylene naphthalate),poly(butylene terephthalate), styrene butadiene rubber, polystyrene,poly(vinyl chloride), poly(vinyl alcohol), poly(vinylidene fluoride),poly(vinyl butylene) and copolymers, derivative compounds, or blendsthereof.
 11. The filtration device of claim 8, wherein the polymercomprises an aliphatic polyamide.
 12. The filtration device of claim 8,wherein the polymer comprises a blend of polymers or copolymers.
 13. Thefiltration device of claim 8, wherein the nanofiber is disposed on aporous support.
 14. The filtration device of claim 13, wherein theporous support comprises one or more layers selected from the groupconsisting of spunbonded nonwovens, meltblown nonwovens, needle punchednonwovens, spunlaced nonwovens, wet laid nonwovens, resin-bondednonwovens, woven fabrics, knit fabrics, paper, and combinations thereof.15. The filtration device of claim 8, wherein the porosity is about 90%.16. The filtration device of claim 8, wherein the filtration medium is amultilayer porous nanofiber containing filtration medium.
 17. Thefiltration device of claim 16, wherein the filtration medium has athickness ranging from about 1 μm to about 500 μm.
 18. The filtrationdevice of claim 16, wherein the electrospun nanofibers are disposed on aporous support.
 19. The filtration device of claim 18, wherein theporous support comprises one or more layers selected from the groupconsisting of spunbonded nonwovens, meltblown nonwovens, needle punchednonwovens, spunlaced nonwovens, wet laid nonwovens, resin-bondednonwovens, woven fabrics, knit fabrics, paper, and combinations thereof.20. The filtration device of claim 16, wherein the filtration medium hasa porosity from about 80% to about 95%.